Abstract

The behavior of cryogenic nitrogen in a room-temperature evaporator six meters long is analyzed. Trapezoid fins are employed to enhance the heat flux supplied by the environment. The steady-state governing equations specified by the mixed parameters are derived from the conservations of momentum and energy. The initial value problem is solved by space integration. The fixed ambient conditions are confirmed by way of the meltback effect. An integrated model is utilized to analyze the convective effect of two-phase flow, which dominates the evaporation behavior. Another integrated model is employed to determine the total heat flux from the environment to the wet surface of the evaporator. The foundation of the formation of an ice layer surrounding the evaporator is presented. If the fin height is shorter than 0.5 m, the whole evaporator is surrounded by ice layer. If the fin height is longer than 0.5 m, the total pressure drop of nitrogen in the tube is negligible. The outlet temperature is always within the range between −12 °C and 16 °C for the evaporator with the fin height of 1.0 m. For the evaporator with dry surface, the nitrogen has the outlet temperature less than the ambient temperature at least by 5 °C.

References

1.
Faghri
,
A.
, and
Zhang
,
Y.
, 2006,
Transport Phenomena in Multiphase Systems
,
Elsevier
,
Houston, Tex
.
2.
Chen
,
I. C.
, 1963, “
A Correlation for Boiling Heat Transfer to Saturated Fluids in Convective Flow
,”
ASME Preprint 63-HT-34
,
Presented at 6th National Heat Transfer Conference
,
Boston, MA
.
3.
Friedel
,
L.
, 1979, “
Improved Friction Pressure Drop Correlations for Horizontal and Vertical Two-Phase Pipe Flow
,” European Two-Phase Flow Group Meeting, Paper E2, Ispra, Italy.
4.
Premoli
,
A.
,
Francesco
,
D.
, and
Prina
,
A.
, 1971, “
A Dimensionless Correlation for Determining the Density of Two-Phase Mixtures
,”
Thermotecnica
,
25
, pp.
17
26
.
5.
Kato
,
H.
,
Shiwaki
,
N. N.
, and
Hirota
,
M.
, 1968, “
On the Turbulent Heat Transfer by Free Convection From a Vertical Plate
,”
Int. Heat Mass Transfer
,
11
, pp.
1117
1125
.
6.
Hewitt
,
G. F.
,
Bott
,
T. R.
, and
Shires
,
G. L.
, 1994,
Process Heat Transfer
,
CRC, Boca Raton
,
FL
.
7.
Hayashi
,
Y.
,
Aoki
,
A.
,
Adachi
,
S.
, and
Hori
,
K.
, 1977, “
Study of Frost Properties Correlating With Frost Formation Types
,”
ASME J. Heat Transfer
,
99
, pp.
239
245
.
8.
Griffith
,
P.
, 1983, “
Dropwise Condensation
,”
Heat Exchange Design Handbook
, Vol.
2
,
Hemisphere
,
New York
.
9.
Stoecker
,
W. F.
, and
Jones
,
J. W.
, 1982,
Refrigeration and Air Conditioning
, 2nd ed.,
McGraw-Hill
,
New York
.
10.
Forster
,
H. K.
, and
Zuber
,
N.
, 1955, “
Dynamics of Vapor Bubbles and Boiling Heat Transfer
,”
AIChE J.
,
1
, pp.
531
535
.
11.
Holman
,
J. P.
, 2001,
Heat Transfer
, 9th ed.,
McGraw-Hill
,
New York
.
12.
Eckert
,
E. R. G.
, and
Drake
,
R. M.
, 1972,
Analysis of Heat and Mass Transfer
,
McGraw-Hill
,
New York
.
You do not currently have access to this content.